JPH05509362A - Chemical pulp bleaching method - Google Patents

Chemical pulp bleaching method

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Publication number
JPH05509362A
JPH05509362A JP3503752A JP50375291A JPH05509362A JP H05509362 A JPH05509362 A JP H05509362A JP 3503752 A JP3503752 A JP 3503752A JP 50375291 A JP50375291 A JP 50375291A JP H05509362 A JPH05509362 A JP H05509362A
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treatment
bleaching
pulp
bleaching method
alkali
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ヴァヘリ、マルヤ
ルオホニエミ、キンモ
ソンニ、ハンヌ
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エンソ―グートツァイト オーワイ
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    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21CPRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C5/00Other processes for obtaining cellulose, e.g. cooking cotton linters ; Processes characterised by the choice of cellulose-containing starting materials
    • D21C5/005Treatment of cellulose-containing material with microorganisms or enzymes
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21CPRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C9/00After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
    • D21C9/10Bleaching ; Apparatus therefor
    • D21C9/1057Multistage, with compounds cited in more than one sub-group D21C9/10, D21C9/12, D21C9/16
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21CPRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C9/00After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
    • D21C9/10Bleaching ; Apparatus therefor
    • D21C9/12Bleaching ; Apparatus therefor with halogens or halogen-containing compounds
    • D21C9/14Bleaching ; Apparatus therefor with halogens or halogen-containing compounds with ClO2 or chlorites
    • D21C9/142Bleaching ; Apparatus therefor with halogens or halogen-containing compounds with ClO2 or chlorites with ClO2/Cl2 in a multistage process involving ClO2/Cl2 exclusively
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21CPRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C9/00After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
    • D21C9/10Bleaching ; Apparatus therefor
    • D21C9/147Bleaching ; Apparatus therefor with oxygen or its allotropic modifications
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21CPRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C9/00After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
    • D21C9/10Bleaching ; Apparatus therefor
    • D21C9/16Bleaching ; Apparatus therefor with per compounds
    • D21C9/163Bleaching ; Apparatus therefor with per compounds with peroxides

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  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Wood Science & Technology (AREA)
  • Chemical & Material Sciences (AREA)
  • Biochemistry (AREA)
  • Microbiology (AREA)
  • Paper (AREA)
  • Investigating Or Analysing Biological Materials (AREA)
  • Hard Magnetic Materials (AREA)
  • Agricultural Chemicals And Associated Chemicals (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるため要約のデータは記録されません。 (57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 ケミカルバルブの漂白方法 本発明は、ケミカルバルブの漂白方法に関し、少なくとも1回の漂白工程、少な くとも1回のアルカリ処理工程およびバルブを酵素で処理することからなる漂白 方法に関する。[Detailed description of the invention] How to bleach chemical valves The present invention relates to a method for bleaching chemical valves, which includes at least one bleaching step and a few bleaching steps. Bleaching consisting of at least one alkaline treatment step and treatment of the valve with enzymes Regarding the method.

とくに硫酸塩法(sulfate cooking )で得られるケミカルバル ブは主としてバルブ中に残存するリグニンにより褐色を呈する。In particular, chemical compounds obtained by sulfate cooking Bulbs take on a brown color mainly due to the lignin remaining in the bulbs.

リグニンは漂白により除去するが、これは通常リグニンを分解する酸化剤で処理 する工程と分解により生した分解生成物を溶解する化学薬品で処理する工程とを 交互に行う多段工程によって行っている。最も普通に使用される酸化剤は塩素含 有物質であり、従つてアルカリ溶液は分解生成物を除去する化学薬品として使用 される。Lignin is removed by bleaching, which is usually treated with an oxidizing agent that breaks down the lignin. and a process of treating the decomposition products produced by the decomposition with chemicals that dissolve them. This is done through a multi-stage process that is performed alternately. The most commonly used oxidizing agents are chlorine-containing therefore, alkaline solutions are used as chemicals to remove decomposition products. be done.

反応に際し、塩素含有漂白剤はバルブ中のリグニンを有機塩素化合物に転化し、 これはバルブから除去される漂白剤廃液中に入り込む。漂白剤廃液はその中に入 り込んだ有機塩素化合物の毒性が強いために環境問題を起こし、また、漂白剤廃 液の化学的酸素消費量の値が高く有害である。During the reaction, the chlorine-containing bleach converts the lignin in the bulb into organochlorine compounds, This enters the bleach waste solution that is removed from the valve. Put the bleach waste in it. The highly toxic organic chlorine compounds introduced into the environment cause environmental problems, and bleach waste The chemical oxygen consumption of the liquid is high and harmful.

環境汚染をもたらす漂白剤廃液は、最初の塩素化とその漂白処理液の最初のアル カリニ程の後の洗浄工程で生じる。この環境汚染を軽減するために、例えば塩素 ガスを二酸化塩素に代えたり、最初の工程での酸化剤として酸素を使用するなど の方法で種々の努力がなされている。しかし、これらの方法では未だ十分満足す べき結果は得られていない。廃液中のクロロフェノール類や他の有毒塩素化合物 の量を減らす努力は確に成功しているが、廃液の化学的酸素消費量の値は減少す るに至らなかった。従って、上記方法を支援するには生物学的な精製を有効に活 用する必要がある。Bleach waste, which causes environmental pollution, undergoes initial chlorination and initial alkaline treatment of the bleaching solution. This occurs during the cleaning process after the carini stage. To reduce this environmental pollution, for example, chlorine For example, replacing the gas with chlorine dioxide or using oxygen as an oxidizing agent in the first step. Various efforts have been made in this way. However, these methods are still not fully satisfactory. The desired results have not been obtained. Chlorophenols and other toxic chlorine compounds in wastewater Efforts to reduce the amount of effluent have certainly been successful; It was not possible to achieve this goal. Therefore, effective use of biological purification is needed to support the above method. It is necessary to use

最近の研究によれば、漂白に際して補助どして酵素を使用することにより、セル ロースからリグニンおよび(または)ヘミセルロースを分離し、かつこの方法で 製造したバルブを次の漂白工程で漂白するのを容易にできることがわかった。フ ランス国特許出[第881192号によれば、塩素化合物を用いて漂白したバル ブ中の残存塩素量は酵素処理により減らすことができる。この場合、酵素処理は 漂白のための酸化およびアルカリニ程の前または後に実施すべきことが開示され ている。Recent research has shown that the use of enzymes to assist in bleaching can Separate lignin and/or hemicellulose from loin and in this way It has been found that the manufactured valves can be easily bleached in a subsequent bleaching step. centre According to Reims Patent No. 881192, balm bleached using chlorine compounds The amount of residual chlorine in the water can be reduced by enzymatic treatment. In this case, the enzyme treatment It is disclosed what should be carried out before or after the oxidation and alkalinization steps for bleaching. ing.

本発明の目的はバルブの酵素処理について新たな方法を提供することにあり、こ の方法によれば、漂白に必要な化学薬品が減少し、同時に漂白剤廃液の化学的酸 素消費量と毒性が減少し、精製に必要な水の量も少なくなるような方法でバルブ の漂白を行うことができる。本発明の特徴は、バルブを2またはそれ以上の漂白 工程で酵素と処理することであり、各酵素処理工程において、バルブはその直前 の工程または直後の工程とは実質的に異なる処理が施される。The purpose of the present invention is to provide a new method for enzymatic treatment of valves. This method reduces the amount of chemicals needed for bleaching and at the same time reduces the chemical acidity of bleach waste. Valve in a way that reduces elemental consumption and toxicity, and also reduces the amount of water required for purification. can be bleached. A feature of the invention is that the bulb can be bleached in two or more ways. In each enzyme treatment process, the valve is placed immediately before the enzyme treatment. Processing that is substantially different from the step or the step immediately following is performed.

本発明によれば、酵素の作用は、いくつかつ異なる工程、好ましくはそのプロセ スに属する酸化工程とアルカリニ程との間で使用したときに、高められることが 観察された。漂白工程の開始時に酵素処理を実施すると、塩素含有化学薬品の使 用量を約25%減らせることが観察された6従ワて本発明による酵素処理を繰り 返すことにより漂白に必要な化学薬品の使用量を大巾に節約することができる。According to the invention, the action of the enzyme is carried out in several different steps, preferably in its process. When used between the oxidation process and the alkaline process belonging to the observed. Enzymatic treatment at the beginning of the bleaching process reduces the use of chlorine-containing chemicals. It was observed that the dose could be reduced by about 25%.6 Therefore, the enzyme treatment according to the present invention was repeated. By recycling, the amount of chemicals needed for bleaching can be significantly reduced.

本発明による漂白方法における好ましい酵素処理工程数は2ないし4工程である 。好ましい方法は、3回の酵素処理工程を含む後、2.Oxカフパ数の比に調整 した。処理温度は40℃、処理時間45分でパルプの含量は3.5%であった。The preferred number of enzyme treatment steps in the bleaching method of the present invention is 2 to 4 steps. . A preferred method includes three enzyme treatment steps, followed by 2. Adjust to the ratio of Ox Kafupa number did. The treatment temperature was 40° C., the treatment time was 45 minutes, and the pulp content was 3.5%.

次いで、比が0.9xカフパの2%の水酸化ナトリウム溶液を用いてパルプをア ルカリ処理した。混合物のコンシスチンシーは10%で、処理温度60℃、処理 時間90分であった。アルカリ処理後、パルプを20倍の水で洗浄した。The pulp is then anointed using a 2% sodium hydroxide solution with a ratio of 0.9x Kafpa. Lucari treated. The consistency of the mixture was 10%, the treatment temperature was 60℃, and the treatment The time was 90 minutes. After the alkali treatment, the pulp was washed with 20 times more water.

その後で、最初の工程と同じ酵素混合物を用いた酵素工程、二酸化塩素を用いた 酸化工程および上記工程間での洗浄を繰り返して行った。この場合、2回目の酵 素処理の酵素量は2.50/g(パルプ)とした。2回目の酸化工程の二酸化塩 素の量は漂白するパルプの量の1.5%とした。This was followed by an enzymatic step using the same enzyme mixture as the first step, followed by an enzymatic step using chlorine dioxide. The oxidation step and the cleaning between the steps were repeated. In this case, the second fermentation The amount of enzyme in the raw treatment was 2.50/g (pulp). Dioxide salt from the second oxidation step The amount of base material was 1.5% of the amount of pulp to be bleached.

漂白したパルプを分析し、その結果を次の表1に示した。The bleached pulp was analyzed and the results are shown in Table 1 below.

上記の実験(実験2)および説明の他に、比較実験(実験1)を行い、その結果 も次の表1に示した。In addition to the above experiment (Experiment 2) and explanation, a comparative experiment (Experiment 1) was conducted, and the results are also shown in Table 1 below.

実験は次のように行った。The experiment was conducted as follows.

実験1 (比較実験):バルブの二回目の酵素処理を行わなかったものである。Experiment 1 (comparative experiment): The second enzyme treatment of the valve was not performed.

他の点は、上述のもの(実験2)と同じである。Other points are the same as those described above (Experiment 2).

表1 実験1 実験2 (比較例) 第1回目酵素処理(酵素比n/l) 1 1C7!0□/C1比 50150  50150カツパ(Kappa ) 27.7 27.7H 酵素工程 5.4 5.6 酸化工程(C10□/CI) 2.1 2.1アルカリニ程 11.7 11. 6 活性塩素の消費(%) 5.54 5.54中間のカッパ 5.7 5.7 第2回目酵素処理(1/l) 0.5 H 第2回目酵素処理 5.3 酸化工程(Color)2.1 2.ISO□工程 開始/終り 4.8 /3 .7 4.8 /3.7白度 60.97 67.54 当業者には、本発明の種々の実施態様が上記の実施例に限定されるものでなく、 添付の請求の範囲の領域内で改変できることは自明であろう。Table 1 Experiment 1 Experiment 2 (Comparative example) 1st enzyme treatment (enzyme ratio n/l) 1 1C7!0□/C1 ratio 50150 50150 Kappa 27.7 27.7H Enzyme process 5.4 5.6 Oxidation step (C10□/CI) 2.1 2.1 Alkalinity 11.7 11. 6 Active chlorine consumption (%) 5.54 5.54 Medium kappa 5.7 5.7 2nd enzyme treatment (1/l) 0.5 H Second enzyme treatment 5.3 Oxidation step (Color) 2.1 2. ISO□Process Start/End 4.8/3 .. 7 4.8 / 3.7 Whiteness 60.97 67.54 Those skilled in the art will appreciate that the various embodiments of the invention are not limited to the above-described examples; It will be obvious that modifications may be made within the scope of the appended claims.

要 約 書 本発明は、ケミカルパルプの漂白方法に関し、1または数回の酸化工程、1また は数回のアルカリ処理工程およびパルプを酵素で処理する漂白方法に関する。本 発明の原理はプロセス中に2回またはそれ以上の工程で酵素で処理し、かつ酵素 処理工程の間で酸化および(または)アルカリ処理を行うことである。使用する 酸化剤でとくに好ましいのは酸素であるが、これに加えてまたはその代わりに過 酸化水素および(または)塩素および(または)二酸化塩素を使用することがで きる。また、酵素処理工程は2〜4回行うのが好ましいが、同一の酵素または2 以上の異なる酵素を交互に使用することもできる。本発明の酵素処理によって、 漂白廃液中の有毒塩素化合物の量が減少すると同時に廃液の化学的酸素消費量も 減少する。Summary book The present invention relates to a method for bleaching chemical pulp, comprising one or several oxidation steps, one or relates to a bleaching method involving several alkaline treatment steps and the treatment of pulp with enzymes. Book The principle of the invention is to treat with enzymes in two or more steps during the process, and Oxidation and/or alkaline treatment is carried out between the treatment steps. use A particularly preferred oxidizing agent is oxygen, but in addition or in place of Hydrogen oxide and/or chlorine and/or chlorine dioxide may be used. Wear. In addition, it is preferable to perform the enzyme treatment step 2 to 4 times, but it is preferable to perform the enzyme treatment step 2 to 4 times. The different enzymes mentioned above can also be used alternately. By the enzyme treatment of the present invention, The amount of toxic chlorine compounds in bleaching effluents is reduced, while the chemical oxygen consumption of the effluents is also reduced. Decrease.

国際調査報告 国際調査報告 1 特表千5−509362 (4)international search report international search report 1 Special Table Sen5-509362 (4)

Claims (10)

【特許請求の範囲】[Claims] (1)最低1回の酸化工程、最低1回のアルカリ処理工程およびパルプを酵素で 処理することを含むケミカルパルプの漂白方法であって、漂白プロセス中パルプ を2またはそれ以上の工程で酵素と処理し、各酵素処理工程に際してパルプをそ の直前または直後のプロセス工程とは実質的に異なる方法を採ることを特徴とす る漂白方法。(1) At least one oxidation process, at least one alkali treatment process, and pulp treatment with enzymes. A method of bleaching chemical pulp comprising: treating the pulp during the bleaching process; is treated with enzymes in two or more steps, and the pulp is treated with enzymes during each enzyme treatment step. characterized by employing a method that is substantially different from the process step immediately before or after bleaching method. (2)2〜4回の別個の酵素処理工程を含む請求の範囲第1項の漂白方法。(2) The bleaching method of claim 1, which comprises 2 to 4 separate enzyme treatment steps. (3)3回の別個の酵素処理工程を含む請求の範囲第2項の漂白方法。(3) The bleaching method of claim 2, which comprises three separate enzyme treatment steps. (4)漂白プロセスの第1工程がパルプの酵素処理であり、次の工程が酸化剤に よるパルプの酸化、第2の酵素処理、アルカリとの処理および第3の酵素処理を 順番に行い、然る後1または数回の酸化および(または)アルカリ処理によりパ ルプの漂白を続行する請求の範囲第3項の漂白方法。(4) The first step in the bleaching process is enzymatic treatment of the pulp, and the next step is the use of an oxidizing agent. oxidation of the pulp, a second enzyme treatment, a treatment with an alkali and a third enzyme treatment. and then one or several oxidation and/or alkali treatments 4. The bleaching method according to claim 3, wherein the bleaching process continues. (5)1または数回のプロセス、工程で使用する酸化剤が酸素である請求の範囲 第1項ないし第4項のいずれかの漂白方法。(5) Claims in which the oxidizing agent used in one or several processes or steps is oxygen. The bleaching method according to any one of paragraphs 1 to 4. (6)プロセス中、少なくとも一つの酵素処理工程の次に、アルカリに対して酸 素または過酸化水素などの酸化剤を添加してアルカリ処理を行う請求の範囲第1 項ないし第5項のいずれかの漂白方法。(6) During the process, after at least one enzymatic treatment step, acid to alkali Claim 1: Alkaline treatment is carried out by adding an oxidizing agent such as hydrogen peroxide or hydrogen peroxide. The bleaching method according to any of Items 5 to 5. (7)プロセスの第1工程が酵素処理であり、次の工程が酸化剤による酸化、第 2の酵素処理、アルカリに酸素または過酸化水素を添加したアルカリ処理、第3 の酵素処理、酸素または二酸化塩素による酸化、アルカリ処理、および酸素また は二酸化塩素による酸化を順番に行う請求の範囲第4項ないし第6項のいずれか の漂白方法。(7) The first step in the process is enzymatic treatment, and the next step is oxidation with an oxidizing agent. 2. Enzyme treatment, alkaline treatment with oxygen or hydrogen peroxide added to alkali, 3. enzymatic treatment, oxidation with oxygen or chlorine dioxide, alkali treatment, and is sequentially oxidized with chlorine dioxide according to any one of claims 4 to 6. bleaching method. (8)使用する酵素がヘミセルラーゼ、セルラーゼ、ペクチナーゼ、エステラー ゼ、リグニナーゼおよび(または)フェノールオキシダーゼである請求の範囲第 1項ないし第7項のいずれかの漂白方法。(8) The enzymes used are hemicellulase, cellulase, pectinase, and esterase. ligninase and/or phenol oxidase. The bleaching method according to any one of Items 1 to 7. (9)最低2回の別個の酵素処理を含み、その中で最低二つの異なる酵素を使用 する請求の範囲第1項ないし第8項のいずれかの漂白方法。(9) includes at least two separate enzymatic treatments, in which at least two different enzymes are used; A bleaching method according to any one of claims 1 to 8. (10)前記プロセスを松の硫酸塩パルプのような針葉樹から得られたパルプの 漂白に適用する請求の範囲第1項ないし第9項のいずれかの漂白方法。(10) The above process can be applied to pulp obtained from softwood such as pine sulfate pulp. A bleaching method according to any one of claims 1 to 9 applied to bleaching.
JP3503752A 1990-02-02 1991-02-01 Chemical pulp bleaching method Pending JPH05509362A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FI900549 1990-02-02
FI900549A FI89814C (en) 1990-02-02 1990-02-02 Process for bleaching cellulose pulp

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JPH05509362A true JPH05509362A (en) 1993-12-22

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EP (1) EP0513140B2 (en)
JP (1) JPH05509362A (en)
AT (1) ATE128498T1 (en)
CA (1) CA2075187A1 (en)
DE (1) DE69113444D1 (en)
ES (1) ES2079062T5 (en)
FI (1) FI89814C (en)
WO (1) WO1991011553A1 (en)

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AU2002229430A1 (en) * 2001-01-18 2002-07-30 Iogen Bio-Products Corporation Use of xylanase in pulp bleaching
WO2003074780A1 (en) * 2002-03-06 2003-09-12 Iogen Bio-Products Corporation Xylanase treatment of chemical pulp
US7547534B2 (en) 2002-06-14 2009-06-16 Verenium Corporation Methods for making a composition to treat a wood, a pulp or a paper
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